The program produces warnings if low
flow velocities will result in slurry particle settlement. For Non-Newtonian
slurries, if shear rates are too low to produce flow, a blocked pipe condition
is simulated in the network with an accompanying warning flag.

Pump Performance Correctionfactors are calculated by the
program depending on slurry particle size, concentration by volume and particle
SG.

Pipe System curves are drawn
showing system resistance curve, settling slurry resistance curve and flow
duty point. For Bingham slurries, the laminar plug flow resistance curve
is drawn This allows you to size each pipe correctly to ensure most economical operation
and to avoid blocked pipe conditions.

Calculate
Fitting Losses using the standard K value method or the Kf method which compensates
for fluid viscosity and turbulence.

Setup individual Fluids and properties
in each pipe - Model real world process lows with different slurries in the same
network. For example, you may
have a concentrated slurry in one pipe flowing into a junction with a water pipe
(or pipes) and dilute slurry flowing through the network from that point onwards.

Include Networks with unknown pressure
nodes and unknown flow nodes or any combination of the two.